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Pretreatment of lignocellulosic biomass for efficient enzymatic saccharification of cellulose  19


               (4) No requirement of biomass size processing to avoid extra energy
                  input for size reduction before the pretreatment.
               (5) Operation  in  reasonable  size  and  moderate  cost  reactors.
                  Pretreatment reactors should be of low cost by minimizing their
                  volumes, using appropriate materials, and keeping operating pressure
                  reasonable.
               (6) Nonproduction of solid residues. Solid-waste formed during the
                  preparation of hydrolyzate should not present processing or disposal
                  challenges.
               (7) Effectiveness at low moisture content. The utilization of low mois-
                  ture content raw material would reduce the energy consumption
                  during pretreatment.
               (8) Obtaining high sugar concentration and fermentation compatibility.
                  The concentration of sugars from pretreatment process and enzyme
                  hydrolysis should be above 10% to ensure an adequate concentration
                  of fermentation product, for example, ethanol, and keep recovery
                  and other downstream costs manageable.
               (9) Lignin recovery. Lignin and other compositions should be recovered
                  and make sure the downstream processing simply and for conversion
                  into valuable coproducts.
              (10) Minimum heat and power requirements. Heat and power are the
                  main energy cost for pretreatment, and low energy consumption is
                  very important for pretreatment.
                 However, it should be noted that to meet all of the abovementioned
              “strict criteria” is impossible, and compromise usually has to be made
              because each pretreatment has its own disadvantages and advantages. To
              combine the merits of different pretreatments, hybrid pretreatment can be
              employed; however, such combination may increase the complicity of the
              process and the cost. In the following sections, the operation modes,
              mechanisms, and enzymatic digestibility of the pretreated substrates will
              be discussed for different pretreatment technologies.




              2.2 Physical pretreatment and mechanisms
              Physical pretreatment aims to increase the surface accessibility of lignocel-
              lulosic biomass to enzymes by reducing the size of the materials or
              destructing the cell wall structure. There are many types of physical pre-
              treatments, but they are generally classified into mechanical comminution
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